CN113019137B - Preparation and application of MXene @ COF composite film - Google Patents
Preparation and application of MXene @ COF composite film Download PDFInfo
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- 239000002131 composite material Substances 0.000 title claims abstract description 46
- 238000002360 preparation method Methods 0.000 title claims abstract description 30
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- 238000000926 separation method Methods 0.000 claims abstract description 20
- 238000000034 method Methods 0.000 claims abstract description 14
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- 239000000203 mixture Substances 0.000 claims description 10
- 230000008569 process Effects 0.000 claims description 9
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- CBCKQZAAMUWICA-UHFFFAOYSA-N 1,4-phenylenediamine Chemical compound NC1=CC=C(N)C=C1 CBCKQZAAMUWICA-UHFFFAOYSA-N 0.000 claims description 8
- 238000006243 chemical reaction Methods 0.000 claims description 8
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- ZXJXZNDDNMQXFV-UHFFFAOYSA-M crystal violet Chemical compound [Cl-].C1=CC(N(C)C)=CC=C1[C+](C=1C=CC(=CC=1)N(C)C)C1=CC=C(N(C)C)C=C1 ZXJXZNDDNMQXFV-UHFFFAOYSA-M 0.000 claims description 2
- JVICFMRAVNKDOE-UHFFFAOYSA-M ethyl violet Chemical compound [Cl-].C1=CC(N(CC)CC)=CC=C1C(C=1C=CC(=CC=1)N(CC)CC)=C1C=CC(=[N+](CC)CC)C=C1 JVICFMRAVNKDOE-UHFFFAOYSA-M 0.000 claims description 2
- DWCZIOOZPIDHAB-UHFFFAOYSA-L methyl green Chemical compound [Cl-].[Cl-].C1=CC(N(C)C)=CC=C1C(C=1C=CC(=CC=1)[N+](C)(C)C)=C1C=CC(=[N+](C)C)C=C1 DWCZIOOZPIDHAB-UHFFFAOYSA-L 0.000 claims description 2
- 229960000907 methylthioninium chloride Drugs 0.000 claims description 2
- JUQPZRLQQYSMEQ-UHFFFAOYSA-N CI Basic red 9 Chemical compound [Cl-].C1=CC(N)=CC=C1C(C=1C=CC(N)=CC=1)=C1C=CC(=[NH2+])C=C1 JUQPZRLQQYSMEQ-UHFFFAOYSA-N 0.000 claims 1
- 229940052223 basic fuchsin Drugs 0.000 claims 1
- 238000001914 filtration Methods 0.000 abstract description 9
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- AXDJCCTWPBKUKL-UHFFFAOYSA-N 4-[(4-aminophenyl)-(4-imino-3-methylcyclohexa-2,5-dien-1-ylidene)methyl]aniline;hydron;chloride Chemical compound Cl.C1=CC(=N)C(C)=CC1=C(C=1C=CC(N)=CC=1)C1=CC=C(N)C=C1 AXDJCCTWPBKUKL-UHFFFAOYSA-N 0.000 description 1
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- 238000005516 engineering process Methods 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 238000002329 infrared spectrum Methods 0.000 description 1
- 239000011229 interlayer Substances 0.000 description 1
- 238000005342 ion exchange Methods 0.000 description 1
- 239000003456 ion exchange resin Substances 0.000 description 1
- 229920003303 ion-exchange polymer Polymers 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
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- 238000005259 measurement Methods 0.000 description 1
- 238000001000 micrograph Methods 0.000 description 1
- 239000002808 molecular sieve Substances 0.000 description 1
- 238000001728 nano-filtration Methods 0.000 description 1
- 150000004767 nitrides Chemical class 0.000 description 1
- 231100000252 nontoxic Toxicity 0.000 description 1
- 230000003000 nontoxic effect Effects 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000002520 smart material Substances 0.000 description 1
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 description 1
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- 229910052723 transition metal Inorganic materials 0.000 description 1
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- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D67/00—Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
- B01D67/0079—Manufacture of membranes comprising organic and inorganic components
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
- B01D69/02—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor characterised by their properties
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- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
- B01D69/12—Composite membranes; Ultra-thin membranes
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- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D71/00—Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
- B01D71/02—Inorganic material
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- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
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- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/30—Organic compounds
- C02F2101/308—Dyes; Colorants; Fluorescent agents
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Abstract
Description
技术领域technical field
本发明属于分离领域,具体涉及MXene@COF复合膜的制备。The invention belongs to the field of separation, and in particular relates to the preparation of MXene@COF composite membranes.
背景技术Background technique
随着工业的快速发展,对有机染料的需求也越来越大。据报道,全球染料产量已超过7×105吨。污水中的有机染料难以降解,对环境和人体健康造成极大危害。因此,开发一种绿色、无毒、高吸附性能的吸附剂具有重要的意义。化学沉淀、离子交换、电化学、膜过滤和吸附是目前公认的去除水溶液中染料的主要方法。其中的化学沉淀会产生大量的浮渣,对其进行严重的处理。离子交换树脂价格昂贵,不能大规模使用。电化学方法既昂贵又低效。膜过滤效率高、能耗小。吸附法设计简单,应用灵活,选择性高,是一种很有前途的吸附技术。With the rapid development of the industry, the demand for organic dyes is also increasing. According to reports, the global dye production has exceeded 7 × 105 tons. Organic dyes in sewage are difficult to degrade and cause great harm to the environment and human health. Therefore, it is of great significance to develop a green, non-toxic and high-adsorption adsorbent. Chemical precipitation, ion exchange, electrochemistry, membrane filtration and adsorption are currently recognized as the main methods for removing dyes from aqueous solutions. The chemical precipitation in it will produce a lot of scum, which will be treated badly. Ion exchange resins are expensive and cannot be used on a large scale. Electrochemical methods are expensive and inefficient. Membrane filtration has high efficiency and low energy consumption. The adsorption method is a promising adsorption technology due to its simple design, flexible application and high selectivity.
COF是一类新型的晶体多孔材料,由共价连接的有机单元组成。由于其独特的特性,例如固有的孔隙率,明确的孔径,有序的通道结构,较大的表面积,出色的热化学稳定性和多种功能,近年来,COF在许多领域引起了极大的关注,包括储气,分子分离,催化,和能量存储。尤其是,COF的独特孔结构在过滤膜中具有高通量的特性,这让其成为构建具有出色性能的分子筛膜的极佳候选者。COFs are a new class of crystalline porous materials composed of covalently linked organic units. Due to their unique properties, such as intrinsic porosity, well-defined pore size, ordered channel structure, large surface area, excellent thermochemical stability, and multiple functions, COFs have attracted tremendous attention in many fields in recent years. concerns, including gas storage, molecular separation, catalysis, and energy storage. In particular, the unique pore structure of COFs provides high-flux properties in filtration membranes, making them an excellent candidate for building molecular sieve membranes with excellent performance.
MXene是基于过渡金属碳化物和/或氮化物的2D新材料系列,由于其复杂,多样的结构,机械,物理和化学特性,其广泛应用于能量存储、智能材料和选择性离子筛领域。MXene膜的层状结构和亲水性可实现水分子和染料分离,但由于Mxene膜的层间距较小,水通量较小,因此限制了它的过滤效率。若能仍将COF与Mxene相结合,既提高复合膜的水通量,又能保持对染料较大的过滤效果,这将极大地提高过滤性能。MXenes are a family of new 2D materials based on transition metal carbides and/or nitrides, which are widely used in the fields of energy storage, smart materials, and selective ion sieves due to their complex, diverse structural, mechanical, physical, and chemical properties. The layered structure and hydrophilicity of MXene membranes can realize the separation of water molecules and dyes, but their filtration efficiency is limited due to the small interlayer spacing and small water flux of MXene membranes. If COF and Mxene can still be combined, the water flux of the composite membrane can be improved, and the filtration effect of dyes can be maintained, which will greatly improve the filtration performance.
发明内容SUMMARY OF THE INVENTION
本发明的目的是针对MXene膜水通量较小的问题,提供一种Mxene/COF复合膜制备方法。本发明利用带正电的COF-LZU1与带负电的Mxene静电自组装的原理,制备得到Mxene/COF复合膜。The purpose of the present invention is to provide a preparation method of Mxene/COF composite membrane in view of the problem of small water flux of MXene membrane. The invention utilizes the principle of electrostatic self-assembly of positively charged COF-LZU1 and negatively charged Mxene to prepare the Mxene/COF composite film.
本发明采用的技术方案如下:The technical scheme adopted in the present invention is as follows:
(1)Ti3C2TX的制备:通过使用含2.0g LiF和40mL HCl(9M)水溶液的蚀刻剂选择性蚀刻2g Ti3AlC2前驱体粉末来制备Ti3C2TX。刻蚀过程在35℃下搅拌,保持24小时,然后将所得的溶液用去离子水洗涤,并以3500rpm的速度离心直至pH达到~5,即得到剥离后的Ti3C2TX片溶液。通过干燥的Ti3C2TX薄膜的重量计算Ti3C2TX浓度。(1) Preparation of Ti 3 C 2 T X : Ti 3 C 2 T X was prepared by selectively etching 2 g of Ti 3 AlC 2 precursor powder using an etchant containing 2.0 g of LiF and 40 mL of aqueous HCl (9M). The etching process was stirred at 35° C. for 24 hours, then the resulting solution was washed with deionized water and centrifuged at 3500 rpm until the pH reached ~5 to obtain a stripped Ti 3 C 2 T X sheet solution. The Ti3C2TX concentration was calculated from the weight of the dried Ti3C2TX thin film.
(2)COF-LZU1的制备:取100mg均苯三甲醛和100mg对苯二胺,溶于20ml二恶烷,然后缓慢加入0.4ml 3mol/L的醋酸溶液,密封静置三天。反应完成后,用甲醇洗涤三次沉淀,然后真空干燥得到COF-LZU1粉末。(2) Preparation of COF-LZU1: Take 100 mg of trimesicaldehyde and 100 mg of p-phenylenediamine, dissolve in 20 ml of dioxane, then slowly add 0.4 ml of 3mol/L acetic acid solution, seal and let stand for three days. After the reaction was completed, the precipitate was washed three times with methanol, and then vacuum-dried to obtain COF-LZU1 powder.
(3)Mxene/COF复合膜的制备:Mxene与COF的总质量固定为3mg,将不同比例的MXene和COF-LZU1共混于20mL的去离子水,然后超声振动10min以分散混合物。充分搅拌MXene和COF溶液(悬浮液)12h后,再超声10min以确保均匀性。制备Mxene/COF复合膜的质量比分别为1:0、8:1、4:1、2:1、1:1、1:2。(3) Preparation of Mxene/COF composite membrane: The total mass of Mxene and COF was fixed at 3 mg. Different proportions of MXene and COF-LZU1 were blended in 20 mL of deionized water, and then ultrasonically vibrated for 10 min to disperse the mixture. After fully stirring the MXene and COF solution (suspension) for 12 h, it was sonicated for another 10 min to ensure homogeneity. The mass ratios of the Mxene/COF composite membranes were 1:0, 8:1, 4:1, 2:1, 1:1, and 1:2, respectively.
优选的是MXene与COF的质量比为1:0、8:1、4:1、2:1、1:1、1:2,在该比例范围内制备的MXene@COF复合膜对染料的过滤效果较好。Preferably, the mass ratio of MXene to COF is 1:0, 8:1, 4:1, 2:1, 1:1, 1:2, and the MXene@COF composite membrane prepared within this ratio range can filter dyes The effect is better.
MXene@COF复合膜的应用,作为分离材料,在染料分离中,通过混合染料溶液选择性分离实验进行测试。即将染料通过复合膜,分析通过前后溶液成分的实验。The application of MXene@COF composite membrane, as a separation material, in dye separation was tested by a mixed dye solution selective separation experiment. That is, the dye is passed through the composite membrane, and the composition of the solution before and after passing through is analyzed.
本发明的MXene@COF复合膜在染料分离中的应用,与之前的相关文献报道相比,具有以下优点:Compared with the previous related literature reports, the application of the MXene@COF composite membrane of the present invention in dye separation has the following advantages:
(1)鉴于MXene膜过滤速度相对较慢,而COF所具有的纳米级多孔结构在过滤速度方面具有优势,通过将Mxene与COF相结合,制备得到MXene@COF复合膜,可以使得Mxene膜克服Mxene膜过滤速度相对较慢的问题;(1) In view of the relatively slow filtration speed of MXene membrane, and the nano-scale porous structure of COF has advantages in terms of filtration speed, by combining Mxene and COF to prepare MXene@COF composite membrane, Mxene membrane can overcome Mxene The problem of relatively slow membrane filtration speed;
(2)Mxene在Ph=7的水溶液中带负电,而COF是带正电,二者通过静电自组装即可实现Mxene和COF的结合,实验过程简单。(2) Mxene is negatively charged in the aqueous solution of Ph=7, while COF is positively charged. The combination of Mxene and COF can be realized by electrostatic self-assembly, and the experimental process is simple.
附图说明Description of drawings
图1为MXene@COF复合膜的红外光谱图;Figure 1 shows the infrared spectrum of the MXene@COF composite film;
图2为MXene@COF复合膜的扫描电镜图;Figure 2 is a scanning electron microscope image of the MXene@COF composite film;
具体实施方式Detailed ways
实施例1Example 1
Ti3C2TX的制备:通过使用含2.0g LiF和40mL HCl(9M)水溶液的蚀刻剂选择性蚀刻2g Ti3AlC2前驱体粉末来制备Ti3C2TX。刻蚀过程在35℃下搅拌,保持24小时,然后将所得的溶液用去离子水洗涤,并以3500rpm的速度离心直至pH达到~5,即得到剥离后的Ti3C2TX片溶液。通过干燥的Ti3C2TX薄膜的重量计算Ti3C2TX浓度。Preparation of Ti3C2TX : Ti3C2TX was prepared by selectively etching 2 g of Ti3AlC2 precursor powder using an etchant containing 2.0 g of LiF and 40 mL of aqueous HCl ( 9M ). The etching process was stirred at 35°C for 24 hours, then the resulting solution was washed with deionized water and centrifuged at 3500 rpm until the pH reached ~5, to obtain a stripped Ti 3 C 2 T X sheet solution. The Ti3C2TX concentration was calculated from the weight of the dried Ti3C2TX thin film.
COF-LZU1的制备:取100mg均苯三甲醛和100mg对苯二胺,溶于20ml二恶烷,然后缓慢加入0.4ml 3mol/L的醋酸溶液,密封静置三天。反应完成后,用甲醇洗涤三次沉淀,然后真空干燥得到COF-LZU1粉末。Preparation of COF-LZU1: Take 100 mg of trimesicaldehyde and 100 mg of p-phenylenediamine, dissolve in 20 ml of dioxane, then slowly add 0.4 ml of 3mol/L acetic acid solution, seal and let stand for three days. After the reaction was completed, the precipitate was washed three times with methanol, and then vacuum-dried to obtain COF-LZU1 powder.
Mxene/COF复合膜的制备:Mxene与COF的总质量固定为3mg,将不同比例的MXene和COF-LZU1共混于20mL的去离子水,然后超声振动10min以分散混合物。充分搅拌MXene和COF溶液(悬浮液)12h后,再超声10min以确保均匀性。制备Mxene/COF复合膜的质量比分别为1:0。Preparation of Mxene/COF composite membrane: The total mass of Mxene and COF was fixed at 3 mg. Different proportions of MXene and COF-LZU1 were blended in 20 mL of deionized water, and then ultrasonically vibrated for 10 min to disperse the mixture. After fully stirring the MXene and COF solution (suspension) for 12 h, it was sonicated for another 10 min to ensure homogeneity. The mass ratios of Mxene/COF composite membranes were 1:0, respectively.
实施例2Example 2
Ti3C2TX的制备:通过使用含2.0g LiF和40mL HCl(9M)水溶液的蚀刻剂选择性蚀刻2g Ti3AlC2前驱体粉末来制备Ti3C2TX。刻蚀过程在35℃下搅拌,保持24小时,然后将所得的溶液用去离子水洗涤,并以3500rpm的速度离心直至pH达到~5,即得到剥离后的Ti3C2TX片溶液。通过干燥的Ti3C2TX薄膜的重量计算Ti3C2TX浓度。Preparation of Ti3C2TX : Ti3C2TX was prepared by selectively etching 2 g of Ti3AlC2 precursor powder using an etchant containing 2.0 g of LiF and 40 mL of aqueous HCl ( 9M ). The etching process was stirred at 35° C. for 24 hours, then the resulting solution was washed with deionized water and centrifuged at 3500 rpm until the pH reached ~5 to obtain a stripped Ti 3 C 2 T X sheet solution. The Ti3C2TX concentration was calculated from the weight of the dried Ti3C2TX thin film.
COF-LZU1的制备:取100mg均苯三甲醛和100mg对苯二胺,溶于20ml二恶烷,然后缓慢加入0.4ml 3mol/L的醋酸溶液,密封静置三天。反应完成后,用甲醇洗涤三次沉淀,然后真空干燥得到COF-LZU1粉末。Preparation of COF-LZU1: Take 100 mg of trimesicaldehyde and 100 mg of p-phenylenediamine, dissolve in 20 ml of dioxane, then slowly add 0.4 ml of 3mol/L acetic acid solution, seal and let stand for three days. After the reaction was completed, the precipitate was washed three times with methanol, and then vacuum-dried to obtain COF-LZU1 powder.
Mxene/COF复合膜的制备:Mxene与COF的总质量固定为3mg,将不同比例的MXene和COF-LZU1共混于20mL的去离子水,然后超声振动10min以分散混合物。充分搅拌MXene和COF溶液(悬浮液)12h后,再超声10min以确保均匀性。制备Mxene/COF复合膜的质量比分别为8:1。Preparation of Mxene/COF composite membrane: The total mass of Mxene and COF was fixed at 3 mg. Different proportions of MXene and COF-LZU1 were blended in 20 mL of deionized water, and then ultrasonically vibrated for 10 min to disperse the mixture. After fully stirring the MXene and COF solution (suspension) for 12 h, it was sonicated for another 10 min to ensure homogeneity. The mass ratio of the prepared Mxene/COF composite films was 8:1, respectively.
实施例3Example 3
Ti3C2TX的制备:通过使用含2.0g LiF和40mL HCl(9M)水溶液的蚀刻剂选择性蚀刻2g Ti3AlC2前驱体粉末来制备Ti3C2TX。刻蚀过程在35℃下搅拌,保持24小时,然后将所得的溶液用去离子水洗涤,并以3500rpm的速度离心直至pH达到~5,即得到剥离后的Ti3C2TX片溶液。通过干燥的Ti3C2TX薄膜的重量计算Ti3C2TX浓度。Preparation of Ti3C2TX : Ti3C2TX was prepared by selectively etching 2 g of Ti3AlC2 precursor powder using an etchant containing 2.0 g of LiF and 40 mL of aqueous HCl ( 9M ). The etching process was stirred at 35° C. for 24 hours, then the resulting solution was washed with deionized water and centrifuged at 3500 rpm until the pH reached ~5 to obtain a stripped Ti 3 C 2 T X sheet solution. The Ti3C2TX concentration was calculated from the weight of the dried Ti3C2TX thin film.
COF-LZU1的制备:取100mg均苯三甲醛和100mg对苯二胺,溶于20ml二恶烷,然后缓慢加入0.4ml 3mol/L的醋酸溶液,密封静置三天。反应完成后,用甲醇洗涤三次沉淀,然后真空干燥得到COF-LZU1粉末。Preparation of COF-LZU1: Take 100 mg of trimesicaldehyde and 100 mg of p-phenylenediamine, dissolve in 20 ml of dioxane, then slowly add 0.4 ml of 3mol/L acetic acid solution, seal and let stand for three days. After the reaction was completed, the precipitate was washed three times with methanol, and then vacuum-dried to obtain COF-LZU1 powder.
Mxene/COF复合膜的制备:Mxene与COF的总质量固定为3mg,将不同比例的MXene和COF-LZU1共混于20mL的去离子水,然后超声振动10min以分散混合物。充分搅拌MXene和COF溶液(悬浮液)12h后,再超声10min以确保均匀性。制备Mxene/COF复合膜的质量比分别为4:1。Preparation of Mxene/COF composite membrane: The total mass of Mxene and COF was fixed at 3 mg. Different proportions of MXene and COF-LZU1 were blended in 20 mL of deionized water, and then ultrasonically vibrated for 10 min to disperse the mixture. After fully stirring the MXene and COF solution (suspension) for 12 h, it was sonicated for another 10 min to ensure homogeneity. The mass ratio of the prepared Mxene/COF composite films was 4:1, respectively.
实施例4Example 4
Ti3C2TX的制备:通过使用含2.0g LiF和40mL HCl(9M)水溶液的蚀刻剂选择性蚀刻2g Ti3AlC2前驱体粉末来制备Ti3C2TX。刻蚀过程在35℃下搅拌,保持24小时,然后将所得的溶液用去离子水洗涤,并以3500rpm的速度离心直至pH达到~5,即得到剥离后的Ti3C2TX片溶液。通过干燥的Ti3C2TX薄膜的重量计算Ti3C2TX浓度。Preparation of Ti3C2TX : Ti3C2TX was prepared by selectively etching 2 g of Ti3AlC2 precursor powder using an etchant containing 2.0 g of LiF and 40 mL of aqueous HCl ( 9M ). The etching process was stirred at 35° C. for 24 hours, then the resulting solution was washed with deionized water and centrifuged at 3500 rpm until the pH reached ~5 to obtain a stripped Ti 3 C 2 T X sheet solution. The Ti3C2TX concentration was calculated from the weight of the dried Ti3C2TX thin film.
COF-LZU1的制备:取100mg均苯三甲醛和100mg对苯二胺,溶于20ml二恶烷,然后缓慢加入0.4ml 3mol/L的醋酸溶液,密封静置三天。反应完成后,用甲醇洗涤三次沉淀,然后真空干燥得到COF-LZU1粉末。Preparation of COF-LZU1: Take 100 mg of trimesicaldehyde and 100 mg of p-phenylenediamine, dissolve in 20 ml of dioxane, then slowly add 0.4 ml of 3mol/L acetic acid solution, seal and let stand for three days. After the reaction was completed, the precipitate was washed three times with methanol, and then vacuum-dried to obtain COF-LZU1 powder.
Mxene/COF复合膜的制备:Mxene与COF的总质量固定为3mg,将不同比例的MXene和COF-LZU1共混于20mL的去离子水,然后超声振动10min以分散混合物。充分搅拌MXene和COF溶液(悬浮液)12h后,再超声10min以确保均匀性。制备Mxene/COF复合膜的质量比分别为2:1。Preparation of Mxene/COF composite membrane: The total mass of Mxene and COF was fixed at 3 mg. Different proportions of MXene and COF-LZU1 were blended in 20 mL of deionized water, and then ultrasonically vibrated for 10 min to disperse the mixture. After fully stirring the MXene and COF solution (suspension) for 12 h, it was sonicated for another 10 min to ensure homogeneity. The mass ratios of the Mxene/COF composite membranes were 2:1, respectively.
实施例5Example 5
Ti3C2TX的制备:通过使用含2.0g LiF和40mL HCl(9M)水溶液的蚀刻剂选择性蚀刻2g Ti3AlC2前驱体粉末来制备Ti3C2TX。刻蚀过程在35℃下搅拌,保持24小时,然后将所得的溶液用去离子水洗涤,并以3500rpm的速度离心直至pH达到~5,即得到剥离后的Ti3C2TX片溶液。通过干燥的Ti3C2TX薄膜的重量计算Ti3C2TX浓度。Preparation of Ti3C2TX : Ti3C2TX was prepared by selectively etching 2 g of Ti3AlC2 precursor powder using an etchant containing 2.0 g of LiF and 40 mL of aqueous HCl ( 9M ). The etching process was stirred at 35° C. for 24 hours, then the resulting solution was washed with deionized water and centrifuged at 3500 rpm until the pH reached ~5 to obtain a stripped Ti 3 C 2 T X sheet solution. The Ti3C2TX concentration was calculated from the weight of the dried Ti3C2TX thin film.
COF-LZU1的制备:取100mg均苯三甲醛和100mg对苯二胺,溶于20ml二恶烷,然后缓慢加入0.4ml 3mol/L的醋酸溶液,密封静置三天。反应完成后,用甲醇洗涤三次沉淀,然后真空干燥得到COF-LZU1粉末。Preparation of COF-LZU1: Take 100 mg of trimesicaldehyde and 100 mg of p-phenylenediamine, dissolve in 20 ml of dioxane, then slowly add 0.4 ml of 3mol/L acetic acid solution, seal and let stand for three days. After the reaction was completed, the precipitate was washed three times with methanol, and then vacuum-dried to obtain COF-LZU1 powder.
Mxene/COF复合膜的制备:Mxene与COF的总质量固定为3mg,将不同比例的MXene和COF-LZU1共混于20mL的去离子水,然后超声振动10min以分散混合物。充分搅拌MXene和COF溶液(悬浮液)12h后,再超声10min以确保均匀性。制备Mxene/COF复合膜的质量比分别为1:1。Preparation of Mxene/COF composite membrane: The total mass of Mxene and COF was fixed at 3 mg. Different proportions of MXene and COF-LZU1 were blended in 20 mL of deionized water, and then ultrasonically vibrated for 10 min to disperse the mixture. After fully stirring the MXene and COF solution (suspension) for 12 h, it was sonicated for another 10 min to ensure homogeneity. The mass ratios of the Mxene/COF composite membranes were 1:1, respectively.
实施例6Example 6
Ti3C2TX的制备:通过使用含2.0g LiF和40mL HCl(9M)水溶液的蚀刻剂选择性蚀刻2g Ti3AlC2前驱体粉末来制备Ti3C2TX。刻蚀过程在35℃下搅拌,保持24小时,然后将所得的溶液用去离子水洗涤,并以3500rpm的速度离心直至pH达到~5,即得到剥离后的Ti3C2TX片溶液。通过干燥的Ti3C2TX薄膜的重量计算Ti3C2TX浓度。Preparation of Ti3C2TX : Ti3C2TX was prepared by selectively etching 2 g of Ti3AlC2 precursor powder using an etchant containing 2.0 g of LiF and 40 mL of aqueous HCl ( 9M ). The etching process was stirred at 35° C. for 24 hours, then the resulting solution was washed with deionized water and centrifuged at 3500 rpm until the pH reached ~5 to obtain a stripped Ti 3 C 2 T X sheet solution. The Ti3C2TX concentration was calculated from the weight of the dried Ti3C2TX thin film.
COF-LZU1的制备:取100mg均苯三甲醛和100mg对苯二胺,溶于20ml二恶烷,然后缓慢加入0.4ml 3mol/L的醋酸溶液,密封静置三天。反应完成后,用甲醇洗涤三次沉淀,然后真空干燥得到COF-LZU1粉末。Preparation of COF-LZU1: Take 100 mg of trimesicaldehyde and 100 mg of p-phenylenediamine, dissolve in 20 ml of dioxane, then slowly add 0.4 ml of 3mol/L acetic acid solution, seal and let stand for three days. After the reaction was completed, the precipitate was washed three times with methanol, and then vacuum-dried to obtain COF-LZU1 powder.
Mxene/COF复合膜的制备:Mxene与COF的总质量固定为3mg,将不同比例的MXene和COF-LZU1共混于20mL的去离子水,然后超声振动10min以分散混合物。充分搅拌MXene和COF溶液(悬浮液)12h后,再超声10min以确保均匀性。制备Mxene/COF复合膜的质量比分别为1:2。Preparation of Mxene/COF composite membrane: The total mass of Mxene and COF was fixed at 3 mg. Different proportions of MXene and COF-LZU1 were blended in 20 mL of deionized water, and then ultrasonically vibrated for 10 min to disperse the mixture. After fully stirring the MXene and COF solution (suspension) for 12 h, it was sonicated for another 10 min to ensure homogeneity. The mass ratios of the Mxene/COF composite membranes were 1:2, respectively.
染料分离(物理分离)实验:分别配制50mg/L的甲基绿、乙基紫、甲基紫、碱性品红、亚甲基蓝溶液,分别取相同的体积的上述染料溶液混合在一起共1000mL,通过使用有效膜面积为13.85cm2的过滤装置通过纳滤法测量Mxene/COF复合膜的过滤性能。工作压力控制在0.1MPa。在测量之前,将过滤系统过滤一段时间直到达到稳定状态。用紫外分光光度计测量吸光度,根据吸光度计算得出剩余染料的浓度。不同的每组实验进行三次,取三次结果的平均值。Dye separation (physical separation) experiment: prepare 50mg/L methyl green, ethyl violet, methyl violet, basic fuchsine, methylene blue solutions, respectively, take the same volume of the above dye solutions and mix together a total of 1000mL, pass through The filtration performance of the Mxene /COF composite membrane was measured by nanofiltration using a filtration device with an effective membrane area of 13.85 cm. The working pressure is controlled at 0.1MPa. The filter system was filtered for a period of time until a steady state was reached before measurement. The absorbance was measured with a UV spectrophotometer, and the concentration of the remaining dye was calculated from the absorbance. Different experiments were performed three times for each group, and the average of the three results was taken.
吸光度和染料浓度会有相对应的方程式,将得到的吸光度代入,即可得到相对应的剩余染料浓度,染料分离率或吸附率(%)=(初始染料浓度-剩余染料浓度)/初始染料浓度。There will be a corresponding equation for absorbance and dye concentration. Substitute the obtained absorbance to obtain the corresponding remaining dye concentration, dye separation rate or adsorption rate (%) = (initial dye concentration - remaining dye concentration) / initial dye concentration .
结果见表1:The results are shown in Table 1:
表1Table 1
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